Synthesis process with amide zymoid method for pressure reduction azeotropy continuous water elimination
A technology of enzymatic synthesis and amides, applied in the direction of fermentation, can solve the problems of aging service life, high investment cost and inability to apply
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example 1
[0013] 90g (1mol) of methoxyacetic acid, 121g (1mol) of racemic phenethylamine and 5g of Novozym 435 were added to 500ml of anhydrous tert-amyl alcohol to form a mixture, then at 55°C, under constant stirring, the reaction 8hr. Then add 100ml of cyclohexane, turn on the vacuum pump, and reduce the pressure of the reaction system to 0.001-0.005MPa, so that the azeotropic mixed steam is evaporated, and the steamed mixed steam is condensed and separated into layers to form a cyclohexane phase and an aqueous phase , the cyclohexane phase automatically returns to the reaction system for recycling. The reaction system continued to maintain the reaction while distilling off, condensing, and refluxing in this state until the volume of the water phase in the water-splitting condenser no longer increased, and continued to maintain the reaction for 4hr. After the reaction is finished, the reaction mixture is filtered to separate the solid enzyme, and then the solvent and the water-carry...
example 2
[0015] 22g of lauric acid, 14g of lysine and 1g of Aspergillus niger-derived lipase were added to 100ml of anhydrous tert-butanol to form a mixture, and then reacted at 36°C for 12hr under constant stirring. Then add 10ml of hexane, turn on the vacuum pump, reduce the pressure of the reaction system to 0.001-0.005MPa, so that the azeotropic mixed steam is evaporated, and the steamed mixed steam is condensed and separated into layers to form a hexane phase and an aqueous phase. The hexane phase automatically returns to the reaction system for recycling. The reaction system continued to maintain the reaction while evaporating, condensing, and refluxing in this state until all lysine solids disappeared in the reaction system, and the volume of the water phase in the water-splitting condenser no longer increased, and continued to maintain the reaction for 4hr. After the reaction is finished, the reaction mixture is filtered to separate the solid enzyme, and then the solvent and th...
example 3
[0018] 135g of L-aspartic acid, 117g of ethyl D-alanine and 1g of neutral protease were added to 100ml of anhydrous tert-butanol to form a mixture, and then reacted at 36°C for 12hr under constant stirring. Then add 10ml of pentane, turn on the vacuum pump, reduce the pressure of the reaction system to 0.01-0.005MPa, so that the azeotropic mixed steam is evaporated, and the steamed mixed steam is condensed and separated to form a pentane phase and an aqueous phase. The alkane phase automatically returns to the reaction system for recycling. The reaction system continued to maintain the reaction while evaporating, condensing, and refluxing in this state until all the shikimic acid solids disappeared in the reaction system, and the volume of the water phase in the water-splitting condenser did not increase any more, and continued to maintain the reaction for 4 hours. After the reaction is finished, the reaction mixture is filtered to separate the solid enzyme, and then the solve...
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